Disclosure of Invention
In view of the problems existing in the prior art, the invention aims to provide a preparation method of oxide dispersion strengthening steel spherical powder for 3D printing, which solves the problem of lack of oxide dispersion strengthening steel powder for high-quality 3D printing, breaks through the bottleneck of the development of the 3D printing oxide dispersion strengthening steel technology, and the obtained powder has sphericity of more than 75D1/da, granularity of 10-100 mu m, fluidity value of less than 20s/50g and oxygen content of less than 3500ppm.
To achieve the purpose, the invention adopts the following technical scheme:
the invention provides a preparation method of oxide dispersion strengthening steel spherical powder for 3D printing, which comprises the following steps:
(1) Mixing the gas atomization prealloy powder and the rare earth oxide powder, and then performing high-energy ball milling to obtain oxide dispersion strengthening steel powder;
(2) Mixing the oxide dispersion strengthening steel powder obtained in the step (1) with a gas flow grinding medium, adding the mixture into a fluidized bed, and discharging air in the fluidized bed to obtain a material-carrying fluidized bed;
(3) Heating the material-carrying fluidized bed obtained in the step (2), introducing mixed gas after the fluidization state of the powder in the material-carrying fluidized bed is stable, controlling the flow of the mixed gas, cooling after the preset reaction time is reached, and obtaining the steel ball-shaped powder from the material-carrying fluidized bed.
The oxide dispersion strengthening steel ball powder for high-quality 3D printing is prepared by utilizing high-energy ball milling and a fluidized bed, and has the advantages of simple preparation process, low production cost, high efficiency, small impurity introduction amount, easy realization of engineering amplification and the like. The preparation of the oxide dispersion strengthening steel powder for high-quality 3D printing is realized by utilizing the synergistic effect between high-energy ball milling and a fluidized bed, the sphericity is more than 75D1/da, the granularity is 10-100 mu m, the fluidity value is less than 20s/50g, and the oxygen content is less than 3500ppm.
In the invention, the mixed gas is introduced into the cooling process for cooling for 10-30min, and then hydrogen is introduced into the cooling process for cooling, wherein the mixed gas is the mixed gas of argon, nitrogen, neon or helium and the like and hydrogen. The flow of nitrogen or inert gas in the mixed gas is 0.4-2m/min, and the flow of hydrogen is 0.1-1m/min. The flow rate of the hydrogen is 0.1-1.5m/min after cooling for 10-30 min.
The high-energy ball milling is a conventional means in the prior art.
As a preferable technical scheme of the invention, the gas atomization prealloy powder in the step (1) comprises a matrix Fe and alloying elements.
Preferably, the alloying element comprises 1 or a combination of at least 2 of Cr, ni, mo, W, ti, zr or Hf.
Preferably, in the gas-atomized prealloy powder in the step (1), the content of the matrix Fe is 40-95.5% by mass, and the balance is an alloy element, for example, 40%, 45%, 50%, 55%, 60%, 65%, 70%, 75%, 80%, 85%, 90%, 95% or 95.5%, etc., but not limited to the listed values, and other non-listed values in the range are equally applicable.
Preferably, the purity of the gas-atomized prealloyed powder in step (1) is > 98%, for example, 98.2%, 98.5%, 98.7%, 99%, 99.2%, 99.6% or 99.8%, etc., but not limited to the recited values, and other non-recited values within this range are equally applicable.
Preferably, the shape of the gas-atomized pre-alloy powder in the step (1) is spherical.
Preferably, the particle size of the gas-atomized prealloyed powder of step (1) is < 150. Mu.m, for example, 149. Mu.m, 147. Mu.m, 145. Mu.m, 142. Mu.m, 140. Mu.m, 135. Mu.m, 130. Mu.m, 125. Mu.m, 120. Mu.m, 115. Mu.m, 110. Mu.m, 105. Mu.m, etc., but not limited to the values recited, other values not recited in the range are equally applicable.
As a preferable technical scheme of the invention, the rare earth oxide powder in the step (1) comprises yttrium oxide powder.
Preferably, the particle size of the rare earth oxide powder in step (1) is less than 500nm, and may be 498nm, 496nm, 494nm, 492nm, 490nm, 488nm, 486nm, 484nm, 482nm, 480nm, 478nm, 476nm, 474nm, 472nm, 470nm, 450nm, 420nm, 400nm, 350nm or 300nm, for example, but not limited to the values recited, and other non-recited values within this range are equally applicable.
Preferably, the purity of the rare earth oxide powder in the step (1) is > 97%, for example, 97%, 97.5%, 98%, 98.2%, 98.5%, 98.7%, 99%, 99.2%, 99.6% or 99.8%, etc., but not limited to the recited values, and other non-recited values within this range are equally applicable.
As a preferred technical solution of the present invention, the mass ratio of the oxide dispersion strengthening steel powder and the air flow grinding medium in the mixing in the step (2) is > 3:1, for example, it may be 3.4:1, 3.6:1, 3.8:1, 4:1, 4.5:1, 5:1 or 6:1, etc., but not limited to the listed values, and other non-listed values in the range are equally applicable.
Preferably, the air flow grinding medium in the step (2) is spherical ceramic powder with higher hardness than oxide dispersion strengthening steel powder.
Preferably, the spherical ceramic powder is 1 or a combination of at least 2 of zirconia, alumina or tungsten carbide.
The particle size of the spherical ceramic powder is preferably 100 to 300. Mu.m, for example, 100 μm, 120 μm, 140 μm, 160 μm, 180 μm, 200 μm, 220 μm, 240 μm, 260 μm, 280 μm, 300 μm, or the like, but not limited to the recited values, and other non-recited values within the range are equally applicable.
The purity of the spherical ceramic powder is preferably > 99.9%, and may be, for example, 99.91%, 99.92%, 99.93%, 99.94%, 99.95%, 99.96%, 99.97%, 99.98%, 99.99%, or the like, but is not limited to the recited values, and other non-recited values within this range are equally applicable.
Preferably, the purity of the spherical ceramic powder is > 99.99%, for example, 99.991%, 99.992%, 99.993%, 99.994%, 99.995%, 99.996%, 99.997%, 99.998% or 99.999%, etc., but not limited to the recited values, and other non-recited values within this range are equally applicable.
Preferably, the material of the fluidized bed in the step (2) comprises high-purity quartz or stainless steel.
Preferably, the purity of the high purity quartz is equal to or greater than 99.5%, for example, 99.5%, 99.6%, 99.7%, 99.8%, or 99.9%, etc., but is not limited to the recited values, and other non-recited values within this range are equally applicable.
Preferably, the air discharged from the fluidized bed in the step (2) is discharged in the form of a protective gas. Wherein the flow rate of the shielding gas is 0.2-2m/min. The charging time of the shielding gas is more than or equal to 50min.
Preferably, the shielding gas comprises nitrogen and/or an inert gas.
Preferably, the purity of the shielding gas is > 99.99%, for example 99.991%, 99.992%, 99.993%, 99.994%, 99.995%, 99.996%, 99.997%, 99.998% or 99.999%, etc., but not limited to the recited values, other non-recited values within this range are equally applicable.
As a preferable technical scheme of the invention, the mixed gas in the step (3) comprises auxiliary gas and reducing gas.
Preferably, the reducing gas in the mixture is 0-30% by volume, and the balance is auxiliary gas, for example, 0%, 5%, 10%, 15%, 20%, 25% or 30%, etc., but not limited to the recited values, and other non-recited values in the range are equally applicable.
Preferably, the auxiliary gas comprises a gas that does not react with the oxide dispersion strengthened steel powder, preferably 1 or a combination of at least 2 of nitrogen, argon, neon or helium.
Preferably, the purity of the auxiliary gas is > 99.99%, for example 99.991%, 99.992%, 99.993%, 99.994%, 99.995%, 99.996%, 99.997%, 99.998% or 99.999%, etc., but not limited to the recited values, other non-recited values within this range are equally applicable.
Preferably, the reducing gas comprises a gas which reacts with the impurity oxide in the oxide dispersion strengthening steel powder in a reducing way, and preferably hydrogen.
Preferably, the purity of the reducing gas is > 99.99%, for example 99.991%, 99.992%, 99.993%, 99.994%, 99.995%, 99.996%, 99.997%, 99.998% or 99.999%, etc., but not limited to the recited values, other non-recited values within this range are equally applicable.
In a preferred embodiment of the present invention, the heating end point temperature in the step (3) is 400 to 850 ℃, and may be 400 ℃, 450 ℃, 500 ℃, 550 ℃, 600 ℃, 650 ℃, 700 ℃, 750 ℃, 800 ℃, or the like, for example, but the end point temperature is not limited to the values recited, and other values not recited in the range are equally applicable.
As a preferable embodiment of the present invention, the flow rate in the step (3) is 0.1-2m/min, for example, 0.1m/min, 0.2m/min, 0.4m/min, 0.6m/min, 0.8m/min, 1m/min, 1.2m/min, 1.4m/min, 1.6m/min, 1.8m/min or 2m/min, etc., but the flow rate is not limited to the recited values, and other non-recited values in the range are equally applicable.
In the invention, after stabilizing for 5-30min, the volume ratio of the auxiliary gas and the reducing gas in the mixed gas in the flow control can also be controlled by respective flow, the flow of the auxiliary gas is controlled to be 0.1-2m/min, and the flow of the reducing gas is controlled to be 0.1-1.5m/min.
As a preferable technical scheme of the invention, the preset reaction time in the step (3) is more than or equal to 15min, for example, 15min, 18min, 20min, 25min, 30min, 35min, 40min, 50min or 60min and the like, but the preset reaction time is not limited to the listed values, and other non-listed values in the range are applicable.
As a preferable embodiment of the present invention, the sphericity of the steel-ball-shaped powder obtained in the step (3) is > 75d1/da, and for example, 76d1/da, 77d1/da, 78d1/da, 79d1/da, 80d1/da, 85d1/da, 90d1/da, 100d1/da, etc., but not limited to the recited values, and other non-recited values within the range are equally applicable.
The particle size of the steel-ball-shaped powder obtained in the step (3) is preferably 10 to 100. Mu.m, for example, 10 μm, 20 μm, 30 μm, 40 μm, 50 μm, 60 μm, 70 μm, 80 μm, 90 μm or 100 μm, etc., but not limited to the values recited, and other values not recited in the range are equally applicable.
Preferably, the fluidity value of the steel ball-shaped powder obtained in the step (3) is less than 20s/50g, and may be, for example, 19s/50g, 18s/50g, 17s/50g, 16s/50g, 15s/50g, 14s/50g, 10s/50g or 5s/50g, etc., but not limited to the recited values, and other non-recited values within the range are equally applicable.
Preferably, the oxygen content of the steel ball-shaped powder obtained in the step (3) is less than 3500ppm, for example, 3400ppm, 3200ppm, 3000ppm, 2500ppm, 2000ppm, 1500ppm, 1000ppm, 500ppm, 100ppm or 10ppm, etc., but not limited to the recited values, other non-recited values within the range are equally applicable.
As a preferable technical scheme of the invention, the preparation method comprises the following steps:
(1) Mixing the gas atomization prealloy powder and the rare earth oxide powder, and then performing high-energy ball milling to obtain oxide dispersion strengthening steel powder;
(2) Mixing the oxide dispersion strengthening steel powder obtained in the step (1) with a gas flow grinding medium, adding the mixture into a fluidized bed, and discharging air in the fluidized bed to obtain a material-carrying fluidized bed;
(3) Heating the carrying fluidized bed obtained in the step (2) and introducing mixed gas, controlling the flow of the mixed gas after the fluidization state of the powder in the carrying fluidized bed is stable, and cooling after the preset reaction time is reached, so as to obtain the steel ball-shaped powder from the carrying fluidized bed;
in the step (2), the mass ratio of the oxide dispersion strengthening steel powder to the air flow grinding medium in the mixing is more than 3:1, and the air flow grinding medium is spherical ceramic powder with the hardness remarkably higher than that of the oxide dispersion strengthening steel powder;
the mixed gas in the step (3) comprises auxiliary gas and reducing gas, wherein the reducing gas accounts for 0-30% by volume percent, the balance is the auxiliary gas, the heating terminal temperature is 400-850 ℃, the flow is 0.1-2m/min, and the preset reaction time is more than or equal to 15min.
Compared with the prior art, the invention has at least the following beneficial effects:
(1) The oxide dispersion strengthening steel powder prepared by the method has the advantages of higher sphericity, good fluidity, low impurity content and the like, meets the technical requirement of 3D investigation, breaks through the technical bottleneck that 3D printing and forming are difficult due to the lack of high-quality oxide dispersion strengthening steel spherical powder, and has sphericity of more than 75D1/da, granularity of 10-100 mu m, fluidity value of less than 20s/50g and oxygen content of less than 3500ppm.
(2) The method has the advantages of simple equipment and process, short treatment period and flow, high efficiency, stable powder quality, low production cost, easy scale-up and continuous operation, good industrialization prospect and the like.
Detailed Description
For a better illustration of the present invention, which is convenient for understanding the technical solution of the present invention, exemplary but non-limiting examples of the present invention are as follows:
example 1
Oxide dispersion strengthening steel powder with the component of Fe-16Cr-0.5Ti-0.5Y is selected as a raw material, the raw material is obtained by high-energy ball milling treatment according to a formula, and an SEM image is shown as in figure 1, so that the powder is in an irregular flat shape, has extremely poor sphericity and fluidity, and cannot be directly subjected to 3D printing.
100g of powder raw material is weighed and added into a fluidized bed, zirconia ceramic particles with the particle size range of 125-250 mu m are used as auxiliary media of an air flow mill, 10g of zirconia powder is weighed and added into the fluidized bed, argon is introduced into the fluidized bed to discharge air in the fluidized bed, and the air speed is 0.6m/min and the time is 60min. Placing the fluidized bed into a resistance furnace, ensuring that a powder raw material flowing area is positioned in a heating constant temperature area, an air inlet/outlet is far away from the heating area, stabilizing for 5min, reducing the flow rate of argon to 0.5m/min, and introducing hydrogen with the flow rate of 0.1m/min; and (3) raising the temperature in the resistance furnace to 600 ℃, observing the fluidization condition of the powder at the temperature raising rate of 10 ℃/min, determining stable fluidization, and then starting the air current grinding spheroidization treatment, wherein the control time is 60min.
After the experiment is finished, the resistance furnace is closed, the fluidized bed is taken out and placed on a fixed table for air cooling, the mixed atmosphere protection of argon and hydrogen is kept, the argon flow is 0.5m/min, the hydrogen flow is 0.1m/min, the hydrogen is stopped to be introduced after 10min, the argon flow is improved to 0.6m/min, after the fluidized bed is air cooled to room temperature, the argon is stopped to be introduced, powder is taken out from the fluidized bed, a standard mesh screen with 150 meshes and a standard mesh screen with 1500 meshes is selected for respectively screening out powder with the particle size not reaching the standard and zirconia powder, the oxide dispersion strengthening steel powder meeting the 3D printing particle size requirement is obtained, the SEM image is shown in figure 2, the morphology of the powder particles is approximately spherical, the particle size distribution range is 5-50 mu m, and the requirements of the 3D printing technology on the shape and the size of the powder raw materials can be obtained after screening.
The sphericity of the powder after the treatment was 78 (d 1/da) as measured by SEM, the flowability was 19.1s/50g as measured by a Hall flow meter, and the oxygen increment was 500ppm.
Example 2
This embodiment 2 is different from embodiment 1 in that: the components of the oxide dispersion strengthening steel powder in the embodiment 1 are converted from Fe-16Cr-0.5Ti-0.5Y ferrite to Fe-18Cr-8Ni-0.5Ti-0.5Y austenite, the air flow grinding time is reduced from 60min to 15min, the experimental temperature is increased from 600 ℃ to 850 ℃, and other experimental conditions are unchanged.
The sphericity of the powder after the treatment was 76 (d 1/da) as measured by SEM, the flowability was 19.8s/50g as measured by a Hall flow meter, and the oxygen increment was 1800ppm. It is explained that the change of the matrix and the components of the oxide dispersion strengthening steel powder does not significantly affect the implementation performance of the method, and the reduction of the air flow grinding time shortens the sphericizing time of the powder, but the increase of the temperature can promote the softening effect of the metal powder and reduce the hardness, thereby strengthening the sphericizing treatment effect of the powder.
Example 3
This embodiment 2 is different from embodiment 1 in that: the auxiliary medium of the jet mill in example 1 was changed from zirconia ceramic particles to tungsten carbide ceramic particles, 100g of the oxide dispersion-strengthened steel powder raw material was weighed, and 20g of the tungsten carbide ceramic particles were weighed because the tungsten carbide ceramic particles had a larger mass than the zirconia powder, and the oxide dispersion-strengthened steel powder raw material and the tungsten carbide ceramic particles were added to the fluidized bed.
The sphericity of the powder after the treatment was 81 (d 1/da) as measured by SEM, the flowability was 18.8s/50g as measured by a Hall flow meter, and the oxygen increment was 400ppm. Tungsten carbide has higher hardness than zirconia, so that the tungsten carbide has better effect when assisting the jet mill.
Application example 1
2000g of the oxide dispersion-strengthened steel powder obtained in example 1 was weighed and 3D-printed using AFS-M120 selective laser melting equipment model number manufactured by beijing brand automatic molding systems limited, with the following parameters: the high-purity argon gas is used for protecting, the oxygen partial pressure is 2000ppm, the laser power is 150W, the laser scanning speed is 500mm/s, the scanning interval is 40 mu m, the powder spreading thickness is 50 mu m, the sample specification is a cube of 10mm multiplied by 10mm, the forming quality and the structure of a 3D printing product of the oxide dispersion strengthening steel spherical powder are characterized by an optical microscope and a scanning electron microscope, as shown in fig. 3 and 4, the defects of holes, cracks and the like are different after the traditional non-spherical oxide dispersion strengthening steel powder is printed, and the 3D printing device of the oxide dispersion strengthening steel powder is obtained by the powder treatment method has few macroscopic defects and good tissue uniformity; as can be seen from fig. 4, a lot of nano-sized spherical oxide dispersion particles can be found in the material structure, the particle size is uniform, the distribution is very uniform, and the oxide dispersion strengthening steel powder obtained by adopting the powder treatment method of the invention can be subjected to 3D printing to obtain the typical nano-oxide dispersion strengthening structure of the oxide dispersion strengthening steel, so that the contradiction that the powder spheroidization/printing performance and the nano-oxide formation quality are difficult to coordinate in other spheroidization technologies is solved.
Comparative example 1
The difference from example 1 was only that the end point temperature of the heating was 900℃and the sphericity of the powder after SEM measurement was 78 (d 1/da), the flowability was 19.8s/50g as measured by a Hall flow meter, and the oxygen increment was 3650ppm. The reason for the excessive increase in oxygen content is that the powder is easily reflected in the residual oxygen in the high purity gas during the high temperature process.
Comparative example 2
The difference from example 1 was only that the flow rate of the control mixture (argon and hydrogen) was 3m/min, the sphericity of the powder after SEM measurement treatment was 72 (d 1/da), and the flowability was 20.2s/50g as measured by a Hall flow rate meter, while the particle size distribution of the powder was changed from 10 to 100 μm to 18 to 100. Mu.m. The reason is that the increase of the air flow reduces the contact frequency between the powder and between the powder and the air flow grinding medium, reduces the air flow grinding efficiency, and simultaneously the excessively high air speed blows out the powder with the particle size smaller than 18 mu m from the air outlet, so that the particle size range of the treated particles is narrowed.
Comparative example 3
The difference from example 1 is only that the flow rate of the control mixture (argon and hydrogen) is 0.03m/min, the sphericity of the powder after SEM measurement is 35 (d 1/da), and the fluidity is close to 0 as measured by a hall flowmeter, because the powder is not fluidized under the low air flow condition, and the fine powder is agglomerated and bonded under the high temperature condition, and finally the air flow grinding effect cannot be realized.
As can be seen from the results of the above examples and comparative examples, the oxide dispersion strengthening steel ball powder prepared by the method has the advantages of higher sphericity, good fluidity, low impurity content and the like, meets the requirements of 3D investigation technology, breaks through the technical bottleneck that the 3D printing and forming are difficult due to the lack of high-quality oxide dispersion strengthening steel ball powder, has sphericity of more than 75D1/da, granularity of 10-100 mu m, fluidity value of less than 20s/50g and oxygen content of less than 3500ppm.
The applicant states that the detailed structural features of the present invention are described by the above embodiments, but the present invention is not limited to the above detailed structural features, i.e. it does not mean that the present invention must be implemented depending on the above detailed structural features. It should be apparent to those skilled in the art that any modifications of the present invention, equivalent substitutions of selected components of the present invention, addition of auxiliary components, selection of specific modes, etc., are within the scope of the present invention and the scope of the disclosure.
The preferred embodiments of the present invention have been described in detail above, but the present invention is not limited to the specific details of the above embodiments, and various simple modifications can be made to the technical solution of the present invention within the scope of the technical concept of the present invention, and all the simple modifications belong to the protection scope of the present invention.
In addition, the specific features described in the above embodiments may be combined in any suitable manner, and in order to avoid unnecessary repetition, various possible combinations are not described further.
Moreover, any combination of the various embodiments of the invention can be made without departing from the spirit of the invention, which should also be considered as disclosed herein.